• 대한환경공학회지
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• 제34권3호
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• pp.149-154
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• 2012

다양한 염기도를 가진 PAC 응집제를 이용한 응집실험에서, 염기도를 낮게 함유하고 있는 PACB (Polymeric Aluminum Chloride Basicity)의 경우 염기도가 높은 PAC 보다 유기물과 인에 응집효율이 높게 나타났다. 저 염기도의 PACB는 고 염기도의 PAC 보다 monomeric Al(III) 가수분해 종을 많이 함유하였다. 하수처리수의 응집에 있어서 전하중화와 sweep floc 형성에 따른 응집효율은 저 염기도의 PACB가 고 염기도의 PAC에 비하여 다소 효과적인 것으로 나타났다. 이에 따라 PACB와 PAC를 이용한 응집실험 결과 $Al_2O_3$ 농도가 유사한 경우 고 염기도의 PAC에 비하여 저 염기도 PACB가 탁도, $COD_{Mn}$ 그리고 TP 및 $PO_4$-P에 대하여 보다 우수한 응집효과를 나타내었다.

• 한국물환경학회지
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• 제22권2호
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• pp.222-229
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• 2006

The treatment performance and operational parameters of a tertiary wastewater treatment process a biological filtration system were investigated. The biological filtration system consisted of a nitrification filter (Fiter 1) and a polishing filter with anoxic and aerobic parts (Filter 2). SS, T-C-BOD, and T-N in effluent were kept stable at less than 3, 5 mg/L, and 5 mgN/L, respectively, under a HRT in Filter (filter-bed) of 0.37~2.3 h. T-N at the outlet of Filter 2 were about 1~5 mgN/L under the condition of LV of 50~202 m/d. In Filter 2, denitrification was accomplished under LV of 50~168 m/d in a 1 m filter-bed. However, the denitrification capacity reached the maximum when the linear velocity was increased to 202 m/d. Relationship between increase in microorganism and headloss was clearer in Filter 2. As a result, the denitrification rate increased from 1.0~2.3 kgN/($m^3-filter-bed{\cdot}d$) as the headloss increased. The COD removal rate was 6.0~9.6 kgCOD/($m^3-filter-bed{\cdot}d$) when operated with Filters 1 and 2. These results mean that captured bacteria contributed a part of COD consumption and denitrification. The maximum nitrification and denitrification rate was 0.5 and 4 kgN/($m^3-filter-bed{\cdot}d$) in Filter 1 and 2.The ratio of backwashing water to the treated water was about 5~10 %. In Filter 1, wasted sludge in backwashing was only 0.7~5.3 gSS/($m^3$-treated water). In Filter 2, added methanol was converted into sludge and its value was 8.0~24 gSS/($m^3$-treated water). These results proved that this process is both convenient to install as tertiary treatment and cost effective to build and operate.

• 환경위생공학
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• 제15권3호
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• pp.50-56
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• 2000

In this study, sewage were treated with operating Two-step Aeration System and conventional activated sludge process together in a condition. At the same HRT 8hr of Two-step Aeration System and Activated Sludge Process, BOD treatment efficiency of 1st sedimentation basin effluent 36.9% by Two-step Aeration system was 12.3% higher than 24.65 by Activated Sludge Process and the COD treatment efficiency 39.8% by two-step Aeration System was 11.6.3% higher than 28.2% by Activated Sludge Process. BOD and COD treatment efficiencies of 2nd sedimentation basin effluent were 88.1% and 85.6% Two-step Aeration System and were 83.8% and 82.3% Activated Sludge Process. In the first treatment, as BOD was relatively removed a lot, F/M ratio 0.17, $0.21{\cdot}BOD/kg{\cdot}MLSS.d$ was maintained by Activated Sludge Process. Therefore it was proved that organic matter treatment efficiency by Two-step Aeration System os Higher than by Activated Sludge Process in a aeration time 8hr. $NH_4^{+}-N$ treatment efficiencies were 55.5% by Two-step Aeration System and 39.75 by Activated sludge Process. $NO_3^{-}-N$ concentration in 2nd. sedimentation basin effluent were 3.33% by Two-step Aeration System and 2.36% by Activated Sludge Process. From this result, Two-step Aeration System was proved more advantageous treatment process for nitrification than Activated Sludge Process. The fluctuation range of BOD, COD and SS concentration in 2nd sedimentation basin effluent $16~33mg/{\ell}$, $15~23mg/{\ell}$ and $14~22mg/{\ell}$ by Two-step Aeration System was smaller than $16~57mg/{\ell}$, $15~25mg/{\ell}$ by Activated sludge Process. Overall the fluctuation range in 2nd sediment basin effluent by was smaller than by Activated Sludge Process. As a result, it is possible for this Two-step Aeration with no facility investment and a little of operation condition change in a conventional sewage treatment plant to get stability and nitrification of treatment water quality.

• Membrane and Water Treatment
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• 제1권3호
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• pp.207-214
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• 2010

Approximately 80% of water used in urban areas reappears as municipal wastewater (MWW). Reclamation of MWW is an attractive proposition under the present scenario of water stressed cities in India. In this paper, we attempted to reclaim MWW using lab-scale hollow- fiber (HF) membrane modules for possible reuse in non-potable applications. Experiments were conducted to evaluate the efficiency of virgin HF ($M_1$) and modified HF ($M_2$) modules. The $M_2$ module consists of HF modified with a skin layer formed through interfacial polymerization of m-phenylenediamine with trimesoyl chloride (MPD-TMC). The molecular weight cut-off (MWCO) of $M_1$ was 44000 g/mol and that of $M_2$ 10000 -14000 g/mol on the basis of rejection of polyethylene glycol. The combination of $M_1$ and $M_2$ modules was able to reduce concentrations of most of the pollutants in sewage and improved the treated water quality to the acceptable limits for non potable reuse applications. It is found that about 98-99% of the initial flux is recovered by the backwashing process, which was approximately two times in a month when operated continuously.

• KSBB Journal
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• 제27권1호
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• pp.16-20
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• 2012

In this study, novel nano silver sand filtration method was compared with UV treatment and normal sand filtration method through filtering treated water from sewage treatment plant. As a result, $BOD_5$ removal rate of nano silver sand filtration showed higher approximately 31% and 23%, comparing with UV treatment and sand filtration. Moreover, $KMnO_4$ removal rate of nano silver sand was about 6.6 and 2.8 times higher than other two methods. In addition, it showed better for removing SS and total coliform, comparing with others. Also, there is no bacteria on nano silver sand after experiments. Therefore, nano silver sand filtration will be effective for advanced water treatment.

• 생태와환경
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• 제33권4호통권92호
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• pp.387-394
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• 2000

경안천의 상${\cdot}$하류와 팔당호 주요 유입부에서 부영양화 양상과 수질오염 특성을 파악하기 위해 2000년 4월부터 7월까지 조사하였다. 경안천 수질은 전형적인 과영양상태를 보였고 상류에 위치한 오${\cdot}$폐수처리장(sewage wastewater treatment plant, SWTP)의 배출수가 본류와 합류된 직후부터 크게 악화되었으며, 이에 대한 영향은 하류의 부영양화에 절대적이었다. 배출수로부터 비롯되는 NH$_{4}$와 SRP 영양염은 하류로 유하하면서 급감하는 반면에 자생유기물의 chl-a는 중류에서 폭발적인 증가를 보였다. 환경요인 중 본류에서 NH$_{4}$, SRP 및 chl-a의 평균농도는 각각 1,343 ${\mu}$g N/l, 1,779 ${\mu}$g P/l 및 188 ${\mu}$g/l였고, 특히 P에 대한 부하가 매우 컸으며 식물플랑크톤 생장에 미치는 영향이 현저하였다. 팔당호 유입부 수질의 비교에서 경안천은 북한강과 남한강의 다른 하천에 비해 오염 수준이 가장 높은 것으로 볼 수 있었다. 결과적으로 볼 때, 경안천 뿐만 아니라 팔당호의 상수원 수질보호를 위해서는 오${\cdot}$폐수 처리수의 점오염원 관리에 대한 대책 마련이 매우 시급한 것으로 판단되었다.

• 한국환경복원기술학회지
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• 제9권3호
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• pp.39-50
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• 2006

In this study, the water quality investigated during 2002s to 2004s for Anyang river and its affluent that was based on biological and chemical methods as well as ecological index of each streams. The improving of water quality and the multiplicity of specious in the most streams except for Anyang, which was due to the improving of water quality and water resource. The seasonal dry states are completely disappeared, but water quality of Anyang main stream was classified as fifth grades water with BIP 8.51~10.00 and BOD 8.16~14.4mg/l in Anyang stream overall. And alpha-mesosaprobic in upper, mid parts and polysaprobic in down parts of Anyang main stream are appeared according to Saprobien system, respectively. The water supply of treated sewage is appeared that upgrading effects of water quality in Anyang main stream and affluents of Anyang city area, but the practical effects of "Saving Anyang River" could not gained because the water quality of other branches in upstream parts than upstream measuring point of Anyang main stream, Wanggok stream Sanbon stream in Gunpo and Eeiwang cities, was not improved.

• 한국토양비료학회지
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• 제19권4호
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• pp.307-314
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• 1986

Sewage Sludge 를 시용하지 않은 토양(W), 6년간 시용한 토양($WS_6$), Sludge와 토양의 혼합물을 1주일동안 incubation한 토양($WS_1$), 그리고 Sewage Sludge(SS)로 부터 추출한 수용성 유기물(WSOF)이 구리(II) 이온과 어떻게 착화합물을 형성하는지를 전자스핀공명분광법(ESR)과 전위차적정법을 이용하여 규명하였다. Cu(II)-WSOF 착화합물은 ESR spectra 상에서 $g_{\perp}$ 값보다 큰 $g_{\amalg}$ 값을 가짐으로서 늘어난 팔면체(elongated octahedron) 배위결합을 하고 있음을 나타내었다. $77^{\circ}K$에서 Cu(II)-SS착물은 anisotropic ESR spectrum을 보인 반면 Cu(II)-W착물은 anisotropic spectrum을 나타내었다. 이러한 결과는 결국 W의 산소공여 리간드가 Cu(II)와 강한 착화합물을 이루는 반면에 SS의 리간드는 Cu(II)와 거의 Chelate를 이루지 않고 있음을 의미한다. 또한 Cu(II)-SS 착화합물의 ESR spectra는 평면상의 네개의 모서리 리간드(예, $COO^-$, $H_2O$, $Cl^-$ 등등)의 각각이 한자리 리간드로서 독립적으로 행동하고 있음을 암시한다. W에서는 방향족 카복실기 같은 산소공여 리간드가 주로 Cu(II)와 결합하고 있는것 같고 SS에서는 Sulfonate, 지방족 카복실기 그리고 질소를 함유하는 리간드가 주요한 결합 site인 것 같다. Cu(II)-SS착화합물과 비교할때 Cu(II)-W로 부터 Cu(II)를 치환하는데 6배정도의 Pyridine 농도가 요구되었다.

• 한국토양비료학회지
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• 제18권1호
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• pp.38-49
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• 1985

Sewage sludge를 시용하지 않은 토양(W), 6년간 시용한 토양($WS_6$), Swedge sludge와 토양의 혼합물을 1 주일동안 incubation한 토양( $WS_1$), 그리고 Sewage sludge (SS)로부터 각각 수용성 유기물을 추출, 정제하고 원소분석, 작용기분석을 함과 동시에 IR, UV-VIS, NMR spectroscopy에 의하여 구조적 특성을 조사하였다. SS는 W보다 H, N, P 함량이 많아서 높은 H/C비와 낮은 C/N비로 특징지워 졌으며 total acidity, carboxyl group, phenolic hydroxyl group 함량의 경우 일반적으로 SS가 가장 높았고 그 다음이 $WS_6$, $WS_1$, 그리고 W가 가장 낮았다. Aromatic character나 aromatic carboxyl group 함량은 W가 가장 크고 SS가 가장 적었으며, Aliphatic proton, aliphatic carboxyl group 함량은 SS가 가장 많고 W가 가장 적었다. 단백질 분해산물은 SS에서 풍부했고 W에서는 검출되지 않았다. NMR spectra는 SS의 수소가 W보다 다양한 functional group에 결합되어 있다는 것을 보여 주었으며 aromatic proton의 구조적 주변환경도 SS가 가장 복잡하고 그 다음이 $WS_1$, $WS_6$, 그리고 W가 비교적 단순함을 보여 주었다.

• 한국해양환경ㆍ에너지학회지
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• 제3권3호
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• pp.41-49
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• 2000

수역의 수질개선을 위하여 생활하수, 산업폐수를 처리할 때 주로 BOD 또는 COD를 저하시키는데 주안점을 두어왔으나 제거되지 않은 질소와 인의 유입으로 인하여 해역은 부영양화가 진행되고 있다. 따라서 향후 수질을 개선하기 위해서는 조류증식의 제한인자인 질소와 인의 처리가 필요하다. 고차처리를 적용할 경우보다 건설비용과 유지관리비가 적게 소요되는 해중방류(Ocean Outfall)을 적용하였을 때 그 효과를 검토하였다. 남부하수처리장 2차처리수를 해중 방류했을 때 수영만 전역에 미치는 영향을 far-field 모델인 생태-유체역학 모델을 이용하여 예측한 결과, 과거 남부하수처리수가 해수면에 유입되던 용호만의 수질은 많은 개선을 보였으나 방류관 주변에서 무기질소와 인의 농도가 해역환경기준 III등급으로 적조나 부영양화의 가능성이 있는 것으로 나타났다.